CN110392606A - For reducing the catalyst for treating waste gas of nitrogen oxides - Google Patents
For reducing the catalyst for treating waste gas of nitrogen oxides Download PDFInfo
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- CN110392606A CN110392606A CN201880013068.XA CN201880013068A CN110392606A CN 110392606 A CN110392606 A CN 110392606A CN 201880013068 A CN201880013068 A CN 201880013068A CN 110392606 A CN110392606 A CN 110392606A
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- 239000003054 catalyst Substances 0.000 title claims abstract description 167
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 title claims abstract description 74
- 239000002912 waste gas Substances 0.000 title description 2
- 229910052751 metal Inorganic materials 0.000 claims abstract description 68
- 239000002184 metal Substances 0.000 claims abstract description 68
- 239000002808 molecular sieve Substances 0.000 claims abstract description 61
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- 239000007789 gas Substances 0.000 claims abstract description 53
- 239000010949 copper Substances 0.000 claims abstract description 32
- 238000000034 method Methods 0.000 claims abstract description 26
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 22
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 22
- 229910052802 copper Inorganic materials 0.000 claims abstract description 22
- 238000010531 catalytic reduction reaction Methods 0.000 claims abstract description 7
- 229910052742 iron Inorganic materials 0.000 claims abstract description 6
- 239000000758 substrate Substances 0.000 claims description 60
- 230000032683 aging Effects 0.000 claims description 54
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- FKTOIHSPIPYAPE-UHFFFAOYSA-N samarium(iii) oxide Chemical compound [O-2].[O-2].[O-2].[Sm+3].[Sm+3] FKTOIHSPIPYAPE-UHFFFAOYSA-N 0.000 description 1
- VSZWPYCFIRKVQL-UHFFFAOYSA-N selanylidenegallium;selenium Chemical compound [Se].[Se]=[Ga].[Se]=[Ga] VSZWPYCFIRKVQL-UHFFFAOYSA-N 0.000 description 1
- 229910052851 sillimanite Inorganic materials 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910052642 spodumene Inorganic materials 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 1
- 229910052645 tectosilicate Inorganic materials 0.000 description 1
- JBQYATWDVHIOAR-UHFFFAOYSA-N tellanylidenegermanium Chemical compound [Te]=[Ge] JBQYATWDVHIOAR-UHFFFAOYSA-N 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 230000001052 transient effect Effects 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
- 229910003454 ytterbium oxide Inorganic materials 0.000 description 1
- 229940075624 ytterbium oxide Drugs 0.000 description 1
- 229910052845 zircon Inorganic materials 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/18—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
- F01N3/20—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
- F01N3/2066—Selective catalytic reduction [SCR]
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/82—Phosphates
- B01J29/84—Aluminophosphates containing other elements, e.g. metals, boron
- B01J29/85—Silicoaluminophosphates [SAPO compounds]
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9404—Removing only nitrogen compounds
- B01D53/9409—Nitrogen oxides
- B01D53/9413—Processes characterised by a specific catalyst
- B01D53/9418—Processes characterised by a specific catalyst for removing nitrogen oxides by selective catalytic reduction [SCR] using a reducing agent in a lean exhaust gas
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9404—Removing only nitrogen compounds
- B01D53/9409—Nitrogen oxides
- B01D53/9413—Processes characterised by a specific catalyst
- B01D53/9422—Processes characterised by a specific catalyst for removing nitrogen oxides by NOx storage or reduction by cyclic switching between lean and rich exhaust gases (LNT, NSC, NSR)
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9445—Simultaneously removing carbon monoxide, hydrocarbons or nitrogen oxides making use of three-way catalysts [TWC] or four-way-catalysts [FWC]
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9459—Removing one or more of nitrogen oxides, carbon monoxide, or hydrocarbons by multiple successive catalytic functions; systems with more than one different function, e.g. zone coated catalysts
- B01D53/9477—Removing one or more of nitrogen oxides, carbon monoxide, or hydrocarbons by multiple successive catalytic functions; systems with more than one different function, e.g. zone coated catalysts with catalysts positioned on separate bricks, e.g. exhaust systems
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
- B01J29/72—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing iron group metals, noble metals or copper
- B01J29/76—Iron group metals or copper
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
- B01J29/72—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing iron group metals, noble metals or copper
- B01J29/76—Iron group metals or copper
- B01J29/763—CHA-type, e.g. Chabazite, LZ-218
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- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
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- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/617—500-1000 m2/g
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- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N13/00—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00
- F01N13/009—Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00 having two or more separate purifying devices arranged in series
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/033—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters in combination with other devices
- F01N3/035—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters in combination with other devices with catalytic reactors, e.g. catalysed diesel particulate filters
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/0807—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents
- F01N3/0814—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by using absorbents or adsorbents combined with catalytic converters, e.g. NOx absorption/storage reduction catalysts
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/101—Three-way catalysts
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/24—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
- F01N3/28—Construction of catalytic reactors
- F01N3/2803—Construction of catalytic reactors characterised by structure, by material or by manufacturing of catalyst support
- F01N3/2825—Ceramics
- F01N3/2828—Ceramic multi-channel monoliths, e.g. honeycombs
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20738—Iron
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20761—Copper
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/50—Zeolites
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B01D2255/00—Catalysts
- B01D2255/90—Physical characteristics of catalysts
- B01D2255/911—NH3-storage component incorporated in the catalyst
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- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/90—Physical characteristics of catalysts
- B01D2255/915—Catalyst supported on particulate filters
- B01D2255/9155—Wall flow filters
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/18—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
- B01J2229/186—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself not in framework positions
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/30—After treatment, characterised by the means used
- B01J2229/36—Steaming
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- F01N2250/00—Combinations of different methods of purification
- F01N2250/12—Combinations of different methods of purification absorption or adsorption, and catalytic conversion
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- F01N2510/00—Surface coverings
- F01N2510/06—Surface coverings for exhaust purification, e.g. catalytic reaction
- F01N2510/063—Surface coverings for exhaust purification, e.g. catalytic reaction zeolites
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
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Abstract
The present invention provides one kind and effectively reduces nitrogen oxides (NOx) selective catalytic reduction (SCR) catalyst, the SCR catalyst includes to use the metal promoted molecular sieve of the metal promoted selected from iron, copper and combinations thereof, and wherein metal is calculated as 2.6 weight % with the total weight of the molecular sieve based on metal promoted with oxide or less amount exists.The present invention also provides catalyst article, exhaust treatment system method and the methods for handling exhaust gas stream, respectively contain SCR catalyst of the invention.SCR catalyst is particularly useful for handling the exhaust gas of lean-burn gasoline engines.
Description
Inventive technique field
Present invention relates generally to gasoline exhaust gas to handle catalyst field, can especially reduce in emissions from engines
NOxCatalyst.
Background of invention
Usually handled with one or more three-way conversions (TWC) automobile catalyst by the useless of gasoline engine driven vehicle
Gas, such catalyst can effectively reduce the discharge of the engine operated under the conditions of the air/fuel of stoichiometry or near it
Nitrogen oxides (NO in objectx), carbon monoxide (CO) and hydrocarbon (HC) pollutant.Lead to the air and fuel of stoichiometric condition
Precise proportions change with the relative scale of carbon in fuel and hydrogen.Air/fuel (A/F) than be in combustion for example including
Air present in combustion engine and quality of fuel ratio.Stoichiometry A/F ratio corresponds to HC fuel (such as gasoline) completely burned
And obtain carbon dioxide (CO2) and water.Therefore, sign of lambda is for indicating the specific A/F ratio by given fuel divided by stoichiometry A/
F ratio as a result, making: λ=1 is stoichiometric mixture, and λ>1 is depleted fuel mixture, and λ<1 is rich in fuel mixture.
The air-fuel of constant variation is provided with the regular price gasoline engine of electronic fuel-injection system and air intake system
Mixture rapidly and continuously recycles between dilute and dense emission.Recently, in order to improve fuel economy, gasoline is fired
Material engine is designed to run under lean conditions." lean conditions ", which refer to, to be supplied in the ignition mixture of such engine
Air and the ratio of fuel be maintained at stoichiometric ratio or more so that the exhaust gas generated is " dilute ", i.e. the oxygen content phase of exhaust gas
To height.The fuel efficiency that lean-burn gasoline direct-injection (GDI) engine provides is had an advantage that can be by carrying out fuel in excess air
It burns and helps to reduce greenhouse gas emission.
The exhaust gas of the vehicle driven by lean-burn gasoline engines is usually handled with TWC catalyst, which effectively subtracts
CO and HC pollutant in the emission of few engine operated under lean conditions.NO must also be reducedxDischarge to meet
Emission regulation standard.However, TWC catalyst is to reduction NO when petrol engine dilute operationxDischarge is not effective.Two kinds
For restoring NOxMost promising technology be ammine selectivity catalytic reduction (SCR) catalyst and poor NOxTrap (LNT).It will
Certain SCR catalysts are challenging for lean-burn gasoline engines, because such expected catalyst is under the conditions of transient state is dilute/dense
Thermal stability is shown at high temperature.This field is continuously needed SCR catalyst, to effectively reduce the NO of lean-burn gasoline enginesx
Discharge, while also showing enough high high-temp stabilities.
Invention summary
The present invention provides one kind and effectively reduces nitrogen oxides (NOx) selective catalytic reduction (SCR) catalyst, wherein
SCR catalyst includes to use the metal promoted molecular sieve of the metal promoted selected from iron, copper and combinations thereof, and wherein metal is to be based on metal
The total weight of molecular sieve is promoted to be calculated as 2.6 weight % or the presence of less amount with oxide.Having determined reduces on molecular sieve
The thermal stability of the SCR catalyst after dilute/dense aging of high temperature can be improved in content of metal.In certain embodiments, metal
Exist with about 2.0 weight % or lower, or about 1.8 weight % or lower, or about 1.5 weight % or lower amount.For example, metal
Can exist with the amount of about 0.5% to about 2.5 weight % or about 0.5% to about 1.8 weight %.In certain embodiments, golden
Category is copper.
The molecular sieve of SCR catalyst can be maximum ring size and double six rings for example with eight Tetrahedral atoms
(d6r) small pore molecular sieve of unit.In some embodiments, molecular sieve is zeolite, for example, with selected from AEI, AFT, AFV,
AFX、AVL、CHA、DDR、EAB、EEI、ERI、IFY、IRN、KFI、LEV、LTA、LTN、MER、MWF、NPT、PAU、RHO、RTE、
The zeolite of the structure type of RTH, SAS, SAT, SAV, SFW, TSC, UFI and combinations thereof.In some embodiments, structure type
It is CHA.Molecular sieve can have in various ranges, the silica of for example, about 5 to about 100 and the molar ratio of aluminium oxide (SAR).
In certain embodiments, SCR catalyst shows about 60% or higher after heat ageing processing at 300 DEG C
NOxConversion ratio, wherein heat ageing processing at 850 DEG C recycle it is dilute/dense under the conditions of in 10% steam in the presence of carry out 5 hours,
Dilute/dense ageing cycle is by 5 minutes air, 5 minutes N2, 5 minutes 4%H2(surplus N2) and 5 minutes N2Composition repeats this four
Step is until reaching the aging duration.In addition, certain embodiments of SCR catalyst exist after the processing of above-mentioned heat ageing
At least about 0.60g/L or higher NH is shown at 200 DEG C3Storage capacity.
On the other hand, the present invention provides a kind of nitrogen oxides (NO effectively reduced in lean-burn gasoline engines exhaust gasx)
Catalyst article, the catalyst article include the substrate carrier for being provided with carbon monoxide-olefin polymeric, wherein carbon monoxide-olefin polymeric
SCR catalyst comprising any embodiment of the present invention.Exemplary substrate carrier includes honeycomb substrates, can be by for example golden
Belong to or ceramics are constituted.Exemplary honeycomb substrate carrier includes flow through substrate or wall-flow filter.Carbon monoxide-olefin polymeric can
To be applied in substrate carrier in the form of carrier coating, and carrier coating may include additional materials, such as selected from titanium dioxide
The adhesive of silicon, aluminium oxide, titanium dioxide, zirconium oxide, ceria or combinations thereof.
Further, the present invention includes a kind of exhaust treatment system, and it includes the lean-burn gasoline hairs for generating exhaust gas stream
Motivation and positioned at lean-burn gasoline engines downstream and with exhaust gas stream be in fluid communication any embodiment of the present invention catalyst
Product.Exhaust treatment system may also include the three-way conversion for example positioned at lean-burn gasoline engines downstream and SCR catalyst upstream
Catalyst (TWC) and poor NOx(wherein one or two of TWC and LNT are in close at least one of trap (LNT)
In link position).
It yet still another aspect, the present invention provides a kind of method for handling the exhaust gas stream from lean-burn gasoline engines, including
Contact exhaust gas stream and the catalyst article of the substrate carrier comprising being provided with carbon monoxide-olefin polymeric, so that reducing exhaust gas
Nitrogen oxides (NO in streamx), wherein the carbon monoxide-olefin polymeric includes the SCR catalyst of any embodiment of the present invention.
The disclosure includes but is not limited to following embodiments.
Embodiment 1: one kind effectively reducing nitrogen oxides (NOx) selective catalytic reduction (SCR) catalyst, the SCR
Catalyst includes the metal promoted molecular sieve for using the metal promoted selected from iron, copper and combinations thereof, and wherein metal based on metal to be promoted
Total weight into molecular sieve is calculated as 2.6 weight % with oxide or less amount exists.
Embodiment 2: the SCR catalyst of any foregoing embodiments, wherein metal is with about 2.0 weight % or lower amount
In the presence of.
Embodiment 3: the SCR catalyst of any foregoing embodiments, wherein metal is with about 1.8 weight % or lower amount
In the presence of.
Embodiment 4: the SCR catalyst of any foregoing embodiments, wherein metal is with about 1.5 weight % or lower amount
In the presence of.
Embodiment 5: the SCR catalyst of embodiment 1, wherein metal is with about 0.5 weight % to the amount of about 2.5 weight %
In the presence of.
Embodiment 6: the SCR catalyst of any one of embodiment 1-3 or 5, wherein metal is with about 0.5 weight % to about
The amount of 1.8 weight % exists.
Embodiment 7: the SCR catalyst of any foregoing embodiments, wherein metal is copper.
Embodiment 8: the SCR catalyst of any foregoing embodiments, wherein molecular sieve is that have eight Tetrahedral atoms
Maximum ring size and double six rings (d6r) unit small pore molecular sieve.
Embodiment 9: the SCR catalyst of any foregoing embodiments, wherein molecular sieve is zeolite.
Embodiment 10: the SCR catalyst of any foregoing embodiments, wherein the structure type of zeolite be selected from AEI, AFT,
AFV、AFX、AVL、CHA、DDR、EAB、EEI、ERI、IFY、IRN、KFI、LEV、LTA、LTN、MER、MWF、NPT、PAU、RHO、
RTE, RTH, SAS, SAT, SAV, SFW, TSC, UFI and combinations thereof.
Embodiment 11: the SCR catalyst of any foregoing embodiments, wherein structure type is CHA.
Embodiment 12: the SCR catalyst of any foregoing embodiments, the wherein silica of molecular sieve and aluminium oxide
Molar ratio (SAR) is about 5 to about 100.
Embodiment 13: the SCR catalyst of any foregoing embodiments, wherein SCR catalyst heat ageing processing after
About 60% or higher NO is shown at 300 DEG CxConversion ratio, wherein heat ageing processing is at 850 DEG C under the conditions of recycling dilute/dense
It is carried out 5 hours in the presence of 10% steam, dilute/dense ageing cycle is by 5 minutes air, 5 minutes N2, 5 minutes 4%H2(surplus is
N2) and 5 minutes N2Composition repeats this four steps until reaching the aging duration.
Embodiment 14: the SCR catalyst of any foregoing embodiments, wherein SCR catalyst heat ageing processing after
At least about 0.60g/L or higher NH is shown at 200 DEG C3Storage capacity, wherein heat ageing processing at 850 DEG C recycle it is dilute/
It is carried out 5 hours in the presence of 10% steam under the conditions of dense, dilute/dense ageing cycle is by 5 minutes air, 5 minutes N2, 5 minutes 4%H2
(surplus N2) and 5 minutes N2Composition repeats this four steps until reaching the aging duration.
A kind of embodiment 15: nitrogen oxides (NO effectively reduced in lean-burn gasoline engines exhaust gasx) catalyst system
Product, the catalyst article include the substrate carrier for being provided with carbon monoxide-olefin polymeric, and wherein carbon monoxide-olefin polymeric includes any
The SCR catalyst of foregoing embodiments.
Embodiment 16: the catalyst article of any foregoing embodiments, wherein substrate carrier is honeycomb substrates.
Embodiment 17: the catalyst article of any foregoing embodiments, wherein honeycomb substrates are metal or ceramics.
Embodiment 18: the catalyst article of any foregoing embodiments, wherein honeycomb substrates carrier is flow type base
Material or wall-flow filter.
Embodiment 19: the catalyst article of any foregoing embodiments, wherein carbon monoxide-olefin polymeric is with carrier coating shape
Formula is applied to substrate carrier, carrier coating also include selected from silica, aluminium oxide, titanium dioxide, zirconium oxide, ceria or
The adhesive of a combination thereof.
Embodiment 20: a kind of exhaust treatment system includes: lean-burn gasoline engines, generates exhaust gas stream；Catalyst
Product, positioned at lean-burn gasoline engines downstream and be in fluid communication with exhaust gas stream, which effectively reduces exhaust gas material
Nitrogen oxides (NO in streamx), which includes the substrate carrier for being provided with carbon monoxide-olefin polymeric, wherein being catalyzed
Agent composition includes the SCR catalyst of any foregoing embodiments.
Embodiment 21: the exhaust treatment system of any foregoing embodiments, also comprising being located under lean-burn gasoline engines
The three-way conversion catalyst (TWC) and poor NO of trip and SCR catalyst upstreamxAt least one of trap (LNT).
Embodiment 22: the exhaust treatment system of any foregoing embodiments, wherein one or two of TWC and LNT
In close link position.
Embodiment 23: a method of exhaust gas stream of the processing from lean-burn gasoline engines, comprising: make exhaust gas stream
It is contacted with the catalyst article of the substrate carrier comprising being provided with carbon monoxide-olefin polymeric to reduce the nitrogen oxygen in exhaust gas stream
Compound (NOx), wherein the carbon monoxide-olefin polymeric includes the SCR catalyst of any foregoing embodiments.
Embodiment 24: the method for any foregoing embodiments further includes making exhaust gas stream and one or more catalyst
Product into contact, the catalyst article include that the three-way conversion positioned at lean-burn gasoline engines downstream and SCR catalyst upstream is urged
Agent (TWC) and poor NOxAt least one of trap (LNT).
By reading attached drawing described in detail below and briefly describing below, these and other features of the disclosure,
Aspect and advantage will become obvious.The present invention includes appointing for the two, three, four, or more in the embodiment above
Any two described in what combination and the disclosure, three, the combinations of four or more features or element, with these features
Or element whether this paper specific embodiment description in clearly combine it is unrelated.The disclosure is intended to read on the whole, makes
Any separable feature or element for obtaining the invention disclosed in what various aspects and embodiment in office should be considered as purport
It can combine, unless the context is clearly stated.It will become obvious by hereafter other aspects and advantages of the present invention.
Brief description
In order to provide the understanding to embodiment of the present invention, with reference to attached drawing, the drawings are not necessarily drawn to scale, and wherein
Appended drawing reference refers to the component of exemplary implementation scheme of the invention.Attached drawing is merely exemplary and should not be construed as limiting this hair
It is bright.
Figure 1A is the perspective view of honeycomb type substrate, which may include carbon monoxide-olefin polymeric of the invention；
Figure 1B is relative to partial cross section Figure 1A amplification and intercepted along the plane parallel with the end face of the carrier of Figure 1A
View, which show the enlarged views of multiple gas flow channels shown in Figure 1A.
Fig. 2 shows the section view of a part of wall-flow filter substrate；
Fig. 3 shows the schematic diagram of an embodiment of the emission treatment systems using catalyst of the present invention.
Fig. 4 is the bar shaped for showing the BET surface area according to the sample of embodiment preparation after air aging and dilute/dense aging
Figure.
Fig. 5 illustrates the igniting test result of SCR catalyst as be shown in the examples；With
Fig. 6 is the NH for showing SCR catalyst as be shown in the examples3The bar chart of storage volume.
Detailed description of the invention
Before describing several exemplary implementation schemes of the invention, it should be understood that the present invention is not limited to middle elaboration is described below
Construction or processing step details.The present invention can have other embodiments and can practice in various ways or real
It applies.
The term used in the disclosure provides defined below.
As used in the specification and the appended claims, singular " one ", "one" and "the" include multiple
Number indicant, unless the context is clearly stated.Thus, for example, referring to that " catalyst " includes two or more catalyst
Mixture etc..
As used herein, term " reduces (abate) " reduction for the amount of meaning, and " reducing (abatement) " means by appointing
The reduction measured caused by what means.
As used herein, term " petrol engine " refers to any of the spark ignition for being designed as running on gasoline
Internal combustion engine.Recently, in order to improve fuel economy, gasoline engines are designed to run under lean conditions.It is " dilute
Sheet part " refers to that the ratio of the air being supplied in the ignition mixture of such engine and fuel is maintained at stoichiometric ratio
More than, so that the exhaust gas generated is " dilute ", i.e. the oxygen content of exhaust gas is relatively high (λ > 1).For example, lean-burn gasoline direct-injection (GDI)
Engine provides fuel efficiency and has an advantage that and can help to reduce greenhouse gas and carrying out fuel combustion in excess air
Body discharge.In one or more embodiments, engine is selected from stoichiometry petrol engine or lean-burn gasoline direct-injection is started
Machine.
As used herein, term " stream " broadly refer to may include solid or liquid particles shape substance flowing gas appoint
What is combined.Term " gaseous stream " or " exhaust gas stream " refer to the stream of gaseous component, such as the emission of engine, can wrap
On-gaseous component, such as drop, solid particle containing entrainment etc..The exhaust gas stream of engine is usually also comprising combustion product, no
Completely burned product, nitrogen oxides, flammable and/or carbonaceous particles shape substance (cigarette ash) and unreacted oxygen and nitrogen.
As used herein, term " refractory metal oxide carriers " and " carrier " refer to following high surface area material,
It is upper to carry additional chemical compound or element.Carrier granular usually has hole and wide pore size distribution greater than 20 angstroms.As herein
It is defined, such refractory metal oxide carriers does not include molecular sieve, especially zeolite.In a particular embodiment, can make
With the refractory metal oxide carriers of high surface area, such as alumina supporting material, also referred to as " gama-alumina " or " activation oxygen
Change aluminium ", it usually shows more than 60 meters squared per gram (" m2/ g ") BET surface area, typically up to about 200m2/ g or higher.
Such activated alumina is usually the γ phase of aluminium oxide and the mixture of δ phase, but also may include η, κ and θ aluminium oxide of significant quantity
Phase.Refractory metal oxides in addition to activated alumina can be used as the carrier of at least some catalyst components in given catalyst.
For example, as it is known that ceria in bulk, zirconium oxide, Alpha-alumina, silica, titanium dioxide and other materials are used for this use
On the way.
As used herein, term " BET surface area " has and is related to for passing through N2The Brunauer of determining adsorption surface area,
Its common meaning of Emmett, Teller method.BET type N also can be used in pore size and pore volume2Absorption or desorption experiment are come
Measurement.
As used herein, term " oxygen storage components " (OSC) refers to multivalent state and can be energetically in reducing condition
It is lower to be reacted with reducing agent such as carbon monoxide (CO) and/or hydrogen, then under oxidative conditions with oxidant such as oxygen or nitrogen oxidation
The entity of object reaction.The example of oxygen storage components includes rare earth oxide, especially ceria, lanthana, praseodymium oxide, oxidation
Neodymium, niobium oxide, europium oxide, samarium oxide, ytterbium oxide, yttrium oxide, zirconium oxide and its mixture.
Term " base metal (base metal) " typically refers to relatively easily to aoxidize when exposed to air and moisture or rotten
The metal of erosion.In one or more embodiments, base metal includes one or more selected from vanadium (V), tungsten (W), titanium (Ti), copper
(Cu), iron (Fe), cobalt (Co), nickel (Ni), chromium (Cr), manganese (Mn), neodymium (Nd), barium (Ba), cerium (Ce), lanthanum (La), praseodymium (Pr), magnesium
(Mg), the base metal of calcium (Ca), zinc (Zn), niobium (Nb), zirconium (Zr), molybdenum (Mo), tin (Sn), tantalum (Ta) and strontium (Sr) or combinations thereof
Oxide.
As used herein, term " platinum group metal " or " PGM " refer to one or more chemistry defined in the periodic table of elements
Element, including platinum, palladium, rhodium, osmium, iridium and ruthenium and their mixture.
Certain SCR catalysts of promoter metals with high load amount show the heat gone on business under dense/dilute cycling condition
Stability.It is without being bound by theory, it is believed that the unstability of the SCR catalyst of for example high Cu and/or Fe load is since zeolite is micro-
Hole) in the approximation of Cu (II) and/or Fe (III) cation, be subjected under rich aging condition at high temperature restore and formed
Ni metal and/or metal Fe nano particle.Under lean conditions, those Ni metals and/or metal Fe substance are with aggregated form oxygen
It is melted into CuO and/or Fe2O3Rather than the Cu of site isolation and/or Fe cation.As a result, zeolite structured successive losses Cu and/or Fe
Cationic substance simultaneously finally collapses.Astoundingly, discovery comprising relatively low Cu and/or Fe load capacity catalyst it is dilute/
Under dense aging, higher thermal stability especially is shown under high temperature (such as 850 DEG C).
Therefore, embodiment according to a first aspect of the present invention provides one kind and effectively reduces in gasoline engine exhaust
NOxCatalyst, the catalyst include with selected from iron, copper and combinations thereof metal promoted metal promoted molecular sieve, wherein
Metal is calculated as 2.6 weight % with the total weight based on metal promoted molecular sieve with oxide or less amount exists.
As used herein, term " selective catalytic reduction " (SCR) refers to nitrogen oxide using nitrogenous reducing agent also
It originally is dinitrogen (N2) catalysis process.As used herein, term " nitrogen oxides " or " NOx" indicate nitrogen oxide.
SCR method is using ammonia catalytic reduction process nitrogen oxides to form nitrogen and water:
4NO+4NH3+O2→4N2+6H2O (standard SCR reaction)
2NO2+4NH3→3N2+6H2O (SCR reacts at a slow speed)
NO+NO2+2NH3→2N2+3H2O (quick SCR reaction)
The catalyst used in SCR method ideally should be able to be under hydrothermal conditions in the use temperature condition of wide scope
Good catalytic activity is kept under (for example, about 200 DEG C to about 600 DEG C or higher).Hydrothermal condition, example are frequently encountered in practice
Such as during soot filter (for removing the component of the exhaust treatment system of particle) regeneration.
Term " molecular sieve " refers to zeolite and other framework materials (such as material of same order elements).Molecular sieve is to be based on opening up
The material of the oxonium ion three-dimensional network of exhibition generally comprises tetrahedral site and has substantially homogeneous pore size distribution, wherein putting down
Equal pore size is usually more than 20 angstroms.Pore size is limited by ring size.According to one or more embodiments, it should be understood that pass through it
Framework types limit molecular sieve, it is intended to embrace any and all zeolites or isotypic framework material, such as SAPO, ALPO and MeAPO,
Ge- silicate, full silica (all-silica) and the similar material with identical framework types.
In general, molecular sieve (such as zeolite) is defined as the alumino-silicate with open three dimensional skeletal structure, by corner-sharing
TO4Tetrahedron composition, wherein T is Al, Si or optionally P.The cation of the charge of counter anion skeleton is loose with skeleton oxygen
It is connected, and remaining pore volume fills hydrone.Non-skeleton cation is usually tradable, and hydrone can be removed.
As used herein, term " zeolite " refers to the specific example of molecular sieve, including silicon and aluminium atom.Zeolite is with phase
When the crystalline material of uniform pore dimensions, the type and amount of the cation for including in the type and zeolite lattice of zeolite are depended on,
Diameter is about 3-10 angstroms.The molar ratio (SAR) of the silica and aluminium oxide of zeolite and other molecular sieves can be in wide scope
Interior variation, but usually two or more.In one or more embodiments, the SAR molar ratio of molecular sieve is about 2 to about 300,
Including about 5 to about 250；About 5 to about 200；About 5 to about 100；About 5 to about 50.In one or more specific embodiments, point
The SAR molar ratio of son sieve is about 10 to about 200, about 10 to about 100, about 10 to about 75, about 10 to about 60, about 10 to about 50；About
15 to about 100, about 15 to about 75, about 15 to about 60, about 15 to about 50；About 20 to about 100, about 20 to about 75, about 20 to about 60,
Or about 20 to about 50.
In a more particular embodiment, refer to that material is limited to not include phosphorus or bone by aluminosilicate zeolite framework types
The molecular sieve of other metals replaced in frame.However, for clarity, as used herein, " aluminosilicate zeolite " does not include aluminium
Phosphate material, such as SAPO, ALPO and MeAPO material, and more broadly term " zeolite " be intended to include alumino-silicate and
Aluminate or phosphate.Term " aluminate or phosphate " refers to another specific example of molecular sieve, including aluminium and phosphate atom.Aluminate or phosphate is
Crystalline material with suitable uniform pore dimensions.
In one or more embodiments, molecular sieve independently includes SiO4/AlO4Tetrahedron passes through common oxygen
Atom is connected to form three-dimensional network.In other embodiments, molecular sieve includes SiO4/AlO4/PO4Tetrahedron.One or more
The molecular sieve of a embodiment can be main according to by (SiO4)/AlO4Or SiO4/AlO4/PO4Tetrahedral rigidity network is formed
The geometry in gap distinguish.The entrance in the gap atom open relative to entrance is formed is by 6,8,10 or 12 annular atoms
It is formed.In one or more embodiments, molecular sieve includes the ring size no more than 12 (including 6,8,10 and 12).
According to one or more embodiments, molecular sieve can be based on the matrix topology for identifying structure by it.In general,
Can be used the zeolite of any framework types, for example, ABW, ACO, AEI, AEL, AEN, AET, AFG, AFI, AFN, AFO, AFR,
AFS、AFT、AFX、AFY、AHT、ANA、APC、APD、AST、ASV、ATN、ATO、ATS、ATT、ATV、AVL、AWO、AWW、BCT、
BEA、BEC、BIK、BOG、BPH、BRE、CAN、CAS、SCO、CFI、SGF、CGS、CHA、CHI、CLO、CON、CZP、DAC、DDR、
DFO、DFT、DOH、DON、EAB、EDI、EEI、EMT、EON、EPI、ERI、ESV、ETR、EUO、FAU、FER、FRA、GIS、GIU、
GME、GON、GOO、HEU、IFR、IFY、IHW、IRN、ISV、ITE、ITH、ITW、IWR、IWW、JBW、KFI、LAU、LEV、LIO、
LIT、LOS、LOV、LTA、LTL、LTN、MAR、MAZ、MEI、MEL、MEP、MER、MFI、MFS、MON、MOR、MOZ、MSO、MTF、
MTN、MTT、MTW、MWF、MWW、NAB、NAT、NES、NON、NPO、NPT、NSI、OBW、OFF、OSI、OSO、OWE、PAR、PAU、
PHI、PON、RHO、RON、RRO、RSN、RTE、RTH、RUT、RWR、RWY、SAO、SAS、SAT、SAV、SBE、SBS、SBT、SFE、
SFF、SFG、SFH、SFN、SFO、SFW、SGT、SOD、SOS、SSY、STF、STI、STT、TER、THO、TON、TSC、UEI、UFI、
The framework types of UOZ, USI, UTL, VET, VFI, VNI, VSV, WIE, WEN, YUG, ZON or combinations thereof.
In one or more embodiments, molecular sieve includes 8 ring aperture aluminosilicate zeolites.As used herein, term
" aperture " is that finger-hole opening is less than about 5 angstroms, for example, about 3.8 angstroms.Phrase " 8- ring " zeolite refers to 8- annular distance opening and double six
Ring secondary building units and the zeolite with cage structure (being formed by the double six rings construction unit connected by 4 rings).One
In a or multiple embodiments, molecular sieve is the small pore molecular sieve of the maximum ring size with eight Tetrahedral atoms.
Zeolite is made of secondary building units (SBU) and compound construction unit (CBU), and has many different skeleton knots
Structure.Secondary building units include at most 16 Tetrahedral atoms and are achiral.Compound construction unit does not need to be non-hand
Property, and not necessarily for the entire skeleton of building.For example, one group of zeolite has single 4- ring (s4r) multiple in its skeleton structure
Close construction unit.In 4 rings, " 4 " indicate the position of tetrahedron silicon and aluminium atom, and oxygen atom is between Tetrahedral atoms.
Other compound construction units include for example single 6 ring (s6r) unit, double 4 ring (d4r) units and double 6 rings (d6r) units.D4r is mono-
Member is formed by connecting two s4r units.D6r unit is formed by connecting two s6r units.In d6r unit, there are 12
A Tetrahedral atoms.The Exemplary zeolite framework types used in certain embodiments include AEI, AFT, AFX, AFV, AVL,
CHA、DDR、EAB、EEI、EMT、ERI、FAU、GME、IFY、IRN、JSR、KFI、LEV、LTA、LTL、LTN、MER、MOZ、MSO、
MWF, MWW, NPT, OFF, PAU, RHO, RTE, RTH, SAS, SAT, SAV, SBS, SBT, SFW, SSF, SZR, TSC, UFI and WEN.
In certain advantageous embodiments, zeolite skeleton be selected from AEI, AFT, AFV, AFX, AVL, CHA, DDR, EAB, EEI, ERI,
IFY, IRN, KFI, LEV, LTA, LTN, MER, MWF, NPT, PAU, RHO, RTE, RTH, SAS, SAT, SAV, SFW, TSC, UFI and
A combination thereof.In other specific embodiments, molecular sieve has the bone selected from CHA, AEI, AFX, ERI, KFI, LEV and combinations thereof
Frame type.In another specific embodiment, molecular sieve has the framework types selected from CHA, AEI and AFX.In one or more
Very in specific embodiment, molecular sieve has CHA framework types.
Zeolite CHA- framework-type molecular sieve includes the naturally occurring zeolites Framework aluminosilicates with following approximate expression
(tectosilicate) mineral: (Ca, Na2,K2,Mg)Al2Si4O12·6H2O (for example, hydration calcium aluminium silicate).Three kinds of synthesis
The zeolite CHA- framework-type molecular sieve of form is described in " the Zeolite Molecular Sieves " of D.W.Breck, by John
Wiley&Sons was published in 1973, was incorporated herein by reference.Three kinds of synthesized forms of Breck report are Zeolite K-
G, is described in J.Chem.Soc., and page 2822 (1956), Barrer etc.；Zeolite D, is described in British patent No.868, and 846
(1961)；Zeolite R is described in United States Patent (USP) No.3, and 030,181, it is incorporated herein by reference.The zeolite of another synthesized form
The synthesis of CHA framework types SSZ-13 is described in United States Patent (USP) No.4, in 544,538, is incorporated herein by reference.Have
A kind of synthesis of synthesized form of the molecular sieve of the silicoaluminophosphate 34 (SAPO-34) of CHA framework types is described in United States Patent (USP)
No.4 in 440,871 and 7,264,789, is incorporated herein by reference.It prepares another with CHA framework types SAPO-44
The method of synthesis of molecular sieve is described in United States Patent (USP) No.6, in 162,415, is incorporated herein by reference.
As described above, molecular sieve may include all alumino-silicates, borosilicate, gallium in one or more embodiments
Silicate, MeAPSO and MeAPO composition.These include but is not limited to SSZ-13, SSZ-62, natural chabazite, zeolite K-G,
Linde D、Linde R、LZ-218、LZ-235、LZ-236、ZK-14、SAPO-34、SAPO-44、SAPO-47、ZYT-6、
CuSAPO-34, CuSAPO-44, Ti-SAPO-34 and CuSAPO-47.
As used herein, term " promotion " refers to different from intrinsic contaminants in molecular sieve, intentionally adds to molecular sieve
Component in material.Therefore, compared with the catalyst of the promotor intentionally added, promotor enhancing catalysis is intentionally added
The activity of agent.In order to promote selective catalyst reduction of nitrogen oxides in the presence of ammonia, in one or more embodiments, make to close
Suitable metal is independently exchanged into molecular sieve.According to one or more embodiments, promote to divide with copper (Cu) and/or iron (Fe)
Son sieve.In specific embodiments, molecular sieve is promoted with copper (Cu).In other embodiments, molecular sieve copper (Cu) and
Iron (Fe) promotes.In further embodiment, molecular sieve is promoted with iron (Fe).
Astoundingly, find low promoter metals content cause catalyst under dilute/dense aging condition at 800 DEG C and with
On, it is highly stable at especially 850 DEG C and higher temperature.In one or more embodiments, the promotor gold of catalyst
Belong to content (calculating with metal oxide) to be that 2.6 weight % or less amount are deposited based on the total weight of metal promoted molecular sieve
, such as metal is with about 2.5 weight % or less, about 2.3 weight % or less, about 1.8 weight % or less, about 1.5 weights
Measure % or less, about 1.2 weight % or less, or embodiment existing for about 1.0 weight % or less amount.Tenor
Exemplary range includes about 0.5 weight % to about 2.5 weight % or about 0.5 weight % to about 1.8 weight %.In one or more
In embodiment, promoter metals content is reported based on non-volatile object.
In certain embodiments, the molecular sieve of metal promoted of the invention shows surprising strong water at high temperature
Thermal stability, such as handle in the presence of under recycling dilute/dense condition (dilute/dense aging) in 10% steam in heat ageing at 850 DEG C
After lower progress 5 hours, wherein dilute/dense ageing cycle is by 5 minutes air, 5 minutes N2, 5 minutes 4%H2(surplus N2) and 5 points
Clock N2Composition repeats this four steps until reaching the aging duration.Particularly, it has been determined that embodiment of the present invention exists
Surprising strong SCR performance and NH are shown after above-mentioned aging process3Storge quality.For example, after such aging process,
Certain embodiments of metal promoted molecular sieve of the present invention provide the about 60% or higher NO at 300 DEG CxConversion ratio (for example,
About 65% or higher at 300 DEG C, about 70% or higher, or about 75% or higher).Further, in such aging process
Later, certain embodiments of metal promoted molecular sieve of the invention provide at least about 0.60g/L or higher at 200 DEG C
NH3Storage capacity (amount about 0.65g/L or higher, about 0.70g/L or higher for example at 200 DEG C, or about 0.75g/L or higher).
Substrate
In one or more embodiments, carbon monoxide-olefin polymeric of the invention is arranged on substrate.As used herein, art
Language " substrate " refers to the monolithic materials for placing catalyst material (usually carrier coating form) thereon.By preparing in a liquid
Slurry comprising specified solids content (such as 30-90 weight %) catalyst, then it is coated on substrate and it is dry with
Carrier coating is provided to form carrier coating.As used herein, term " carrier coating " is applied to substrate material such as honeycomb at it
The catalysis of type support element (it allows the gas streams handled to pass through with enough porosity) or the thin of other materials are glued
There is its common meaning in attached coatings art.
Carrier coating comprising metal promoted molecular sieve of the invention optionally including selected from silica, aluminium oxide,
The adhesive of titanium dioxide, zirconium oxide, ceria or combinations thereof.The load capacity of adhesive is typically based on carrier coating weight
About 0.1-10 weight %.
In one or more embodiments, substrate be selected from one of flow type honeycomb-type monolith or particulate filter or
It is a variety of, and catalysis material is applied to substrate as carrier coating.
Figure 1A and 1B shows the exemplary substrate 2 for being coated with the flow through substrate form of carbon monoxide-olefin polymeric described herein.
With reference to Figure 1A, exemplary substrate 2 has 8 (its of cylindrical shape and cylindrical outer surface 4, upstream face 6 and corresponding downstream end face
It is identical as end face 6).Substrate 2 has multiple thin parallel gas flow channels 10 wherein formed.As shown in Figure 1B, flow channel
10 are formed by wall 12 and extend to downstream end face 8 from upstream face 6 by carrier 2, and wherein channel 10 is unobstructed to allow to flow
Body (such as gas streams) flows through carrier 2 longitudinally through its gas flow channel 10.As being more easily seen in fig. ib,
Wall 12 is sized and configured so that gas flow channel 10 has the polygonal shape of primitive rule.As shown in the figure, if it is desired,
Carbon monoxide-olefin polymeric can be coated in multiple and different layers.In the embodiment illustrated, carbon monoxide-olefin polymeric is by being adhered to
It the discrete bottom 14 of the wall 12 of support element and is formed coated on the second discrete top layer 16 on bottom 14.The present invention can be with one
Kind or multiple catalysts layer (such as 2,3 or 4) are implemented, and are not limited to dual layer embodiment shown in Figure 1B.
In one or more embodiments, substrate is the ceramics or metal with honeycomb.Any conjunction can be used
Suitable substrate, such as with the type in the thin parallel gas flow channel wherein extended through from the entrance of substrate or exit face
Monolith substrate so that channel opener is so that fluid flows through wherein.As substantially from its fluid inlet to its stream
The straight line path of body outlet, channel are limited by wall, and catalysis material is coated on the wall as carrier coating, so that flowing through logical
The gas in road is contacted with catalysis material.The flow channel of monolith substrate is thin-walled channels, can have any suitable section shape
Shape and size, such as trapezoidal, rectangle, square, sinusoidal, hexagon, ellipse, circle etc..The class formation is per square inch
Section can include about 60 to about 900 or more gas access openings (i.e. unit).
Ceramic base material can be made of any suitable refractory material, such as cordierite, cordierite-Alpha-alumina, nitridation
Silicon, zirconium mullite, spodumene, alumina-silica magnesia, zirconium silicate, sillimanite, magnesium silicate, zircon, petalite,
Alpha-alumina, alumino-silicate etc..The substrate that can be used for the catalyst of embodiment of the present invention is substantially also possible to metal, and
And it can be made of one or more metal or metal alloy.Metal base may include any metal base, such as in conduit wall
In there is those of opening or " perforation (punched-out) ".Metal base can be used with various shape, such as pellet, wave
Card or monolithic form.The specific example of metal base includes heat-resisting lowpriced metal alloy, and especially wherein iron is significant component
Or those of main component.Such alloy may include one of nickel, chromium and aluminium or a variety of, and the total amount of these metals is in every kind of feelings
Weight under condition based on substrate can advantageously comprise the alloy of at least about 15 weight %, for example, about chromium of 10-25 weight %, about 1-
The aluminium of 8 weight % and the nickel of about 0-20 weight %.
In one or more embodiments that substrate is particulate filter, particulate filter can be selected from diesel particulate filter
Device or soot filter.As used herein, term " particulate filter " or " soot filter ", which refer to, is designed for from exhaust gas material
The filter of particulate matter such as cigarette ash is removed in stream.Particulate filter includes but is not limited to honeycomb wall flow filters device, part mistake
Filter filter, wire gauze filter, winding fabric filter, sintered metal filter and foam filter.It is embodied at one
In scheme, particulate filter is catalysis soot filter (CSF).The CSF of catalysis is including, for example, being coated with for NO to be oxidized to
NO2Inventive catalyst composition substrate.
It can be used for loading the wall stream substrate of the catalyst material of one or more embodiments with multiple along the substrate longitudinal axis
The thin substantially parallel gas flow channel extended.In general, each channel is blocked in one end of substrate body, wherein alternate channel
Block in opposite end face.The section of such monolith substrate per square inch may comprise up to about 900 or more flow channel
(or " unit "), but less flow channel can be used.For example, substrate can have about 7-600 per square inch (" cpsi "),
More typically from about 100-400 unit.It can be catalyzed the porous wall-flow filter for embodiment of the present invention, because of the member
The wall of part has platinum group metal or on it wherein comprising platinum group metal.Catalysis material can separately exist in entering for substrate walls
Both mouth side, individual outlet side, entrance side and outlet side or wall itself can be entirely or partly by catalysis material groups
At.In another embodiment, the present invention may include on the entrance of substrate and/or exit wall using one or more catalyst
The combination of layer and one or more catalyst layers.
As shown in Fig. 2, exemplary substrate has multiple channels 52.It is closed by 53 tubulose of inner wall of filter base material in channel.
Substrate has arrival end 54 and outlet end 56.There is portal plug 58 in replacement channel in arrival end blocking, and blocking has out in outlet end
Mouth plug 60, to form opposite checkerboard pattern at entrance 54 and outlet 56.Gas streams 62 pass through unplugged feeder connection
64 enter, and are stopped by spout plug 60 and diffuse to outlet side 66 by conduit wall 53 (it is porous).Due to portal plug 58, gas
Body cannot lead to the entrance side for being back to wall.It can be catalyzed for porous wall-flow filter of the invention, because substrate walls are on it
With one or more catalysis materials.
Exhaust treatment system
Another aspect of the present invention relates to a kind of exhaust treatment systems.In one or more embodiments, exhaust-gas treatment
System includes petrol engine, especially lean-burn gasoline engines, and the catalyst combination of the present invention positioned at engine downstream
Object.
A kind of exemplary discharge treating system is shown in Fig. 3, which depict the schematic diagrames of discharge treating system 20.Such as figure
Shown, discharge treating system may include concatenated multiple catalyst groups positioned at such as lean-burn gasoline engines downstream of engine 22
Point.At least one catalytic component is the SCR catalyst of invention as described herein.Inventive catalyst composition can be with many
Extra catalyst material combination, and different location can be located at compared with extra catalyst material.Fig. 3 shows concatenated 5 kinds
Catalytic component 24,26,28,30,32；However, the sum of catalytic component can change, and 5 kinds of components are only a reality
Example.
In the absence of constraints, table 1 has the various exhaust treatment systems construction of one or more embodiments.It should be noted that each
Catalyst is connect by exhaust pipe with next catalyst, so that engine is located at the upstream of catalyst A, catalyst A is located at catalysis
The upstream of agent B, catalyst B are located at the upstream of catalyst C, and catalyst C is located at the upstream of catalyst D, and catalyst D is located at catalyst
The upstream of E (when it is present).Reference can be interacted with the same names in Fig. 3 to the instruction of component A-E in table.
TWC catalyst described in table 1 can be conventionally used for reduce engine exhaust gas in carbon monoxide (CO) and
Hydrocarbon (HC) pollutant and being capable of antioxidant nitroxide (NO under certain conditionsx) any catalyst, and generally comprise load
Platinum group metal (PGM) on oxygen storage components (such as ceria) and/or refractory metal oxide carriers (such as aluminium oxide).
TWC catalyst also may include the base metal being impregnated on carrier.
LNT catalyst described in table 1, which can be, is conventionally used as NOxAny catalyst of trap, and generally comprise
NOxAdsorbent composition comprising base metal oxide (BaO, MgO, CeO2Deng) and for be catalyzed NO oxidation and reduction platinum family
Metal (such as Pt and Rh).
The TWC-LNT referred in table refers to that the carbon monoxide-olefin polymeric with TWC and LNT degree of functionality (such as has on substrate
There are the TWC and LNT catalyst composition of stratified form or random mixed form).
The SCR referred in table refers to SCR catalyst, may include SCR catalyst composition of the invention.Refer to SCRoF
(or SCR on filter) refers to particle or soot filter (such as wall-flow filter), may include that SCR of the invention is urged
Agent composition.There are SCR and SCRoF, one or two may include SCR catalyst of the invention, or urge
One of agent may include conventional scr catalyst (such as SCR catalyst with common metal load level).
The FWC referred in tableTM(or four-way catalyst) refers to TWC catalyst and particulate filter (such as wall-flow type mistake
Filter) combination BASF catalyst trade name.
The AMOx referred in table refers to ammoxidation catalyst, can be provided in one or more embodiments of the invention
Catalyst downstream, to remove the ammonia of any escape from exhaust treatment system.In specific embodiments, AMOx is catalyzed
Agent may include PGM component.In one or more embodiments, AMOx catalyst may include having the priming coat of PGM and having
The top coating of SCR function.
As recognized by those skilled in the art, any in component A, B, C, D or E in the construction listed in table 1
One or more can be set on particulate filter (such as wall-flow filter) or flow type monolith substrate.At one or more
In a embodiment, engine exhaust system includes the position being mounted near engine (in close link position, CC)
One or more carbon monoxide-olefin polymerics, wherein additional catalyst composition is located at the position below car body (in underground position, UF).
For example, in certain embodiments, one or two of TWC and LNT are in the position CC, and remaining component is UF.
Table 1
| Component A | Component B | Component C | Component D | Component E |
| TWC | LNT | SCR | Optional AMOx | - |
| TWC | LNT | SCRoF | Optional AMOx | - |
| TWC | LNT | SCRoF | SCR | Optional AMOx |
| TWC | LNT | FWC | SCR | Optional AMOx |
| TWC | TWC-LNT | SCR | Optional AMOx | - |
The method for handling emissions from engines
Another aspect of the present invention relates to the exhaust gas streams of a kind of processing petrol engine, especially lean-burn gasoline engines
Method.This method may include that the catalyst of one or more embodiments in accordance with the present invention is placed under petrol engine
Trip, and flow engine exhaust stream on a catalyst.In one or more embodiments, this method further includes institute as above
It states and places additional catalyst components in engine downstream.
The present invention is now described according to following embodiment.Before describing several exemplary implementation schemes of the invention, Ying Li
The present invention is not limited to the details of construction or processing step described in being described below for solution.The present invention can have other embodiments
And it can be practiced or carried out in various ways.
Embodiment
Embodiment 1- comparison
3.2%CuO Cu-SSZ-13: NH is added in equipped with mechanical agitator and steam-heated container4 +Exchange
SSZ-13 suspension, wherein silica and alumina ratio are 30.Container contents are heated to 60 DEG C under stiring.To anti-
It answers and copper acetate solution is added in mixture.Filter solid is crossed, is washed with deionized, and is air-dried.Gained Cu-SSZ-13 is existed
It is calcined 6 hours at 550 DEG C in air.The copper content of products therefrom is 3.2 weight % based on the CuO measured by icp analysis.
Embodiment 2
2.4%CuO Cu-SSZ-13: it according to the preparation procedure of embodiment 1, obtains copper content and is based on surveying by icp analysis
Fixed CuO is the Cu-SSZ-13 of 2.4 weight %.
Embodiment 3
1.7%CuO Cu-SSZ-13: it according to the preparation procedure of embodiment 1, obtains copper content and is based on surveying by icp analysis
Fixed CuO is the Cu-SSZ-13 of 1.7 weight %.
Embodiment 4
1.1%CuO Cu-SSZ-13: it according to the preparation procedure of embodiment 1, obtains copper content and is based on surveying by icp analysis
Fixed CuO is the Cu-SSZ-13 of 1.1 weight %.
Embodiment 5
0.6%CuO Cu-SSZ-13: it according to the preparation procedure of embodiment 1, obtains copper content and is based on surveying by icp analysis
Fixed CuO is the Cu-SSZ-13 of 0.6 weight %.
Embodiment 6
1.7%CuO CuSAPO-34: according to the preparation procedure of embodiment 3 and with NH4 +- SAPO-34 is used as precursor, obtains
The CuSAPO-34 that copper content is 1.7 weight % based on the CuO measured by icp analysis.
Embodiment 7- aging and test
The aging in the horizontal pipe furnace for being equipped with quartz ampoule by powder sample.Aging is deposited at 850 DEG C in 10% steam
It is carried out 5 hours under air stream (air aging) or dilute/dense condition (dilute/dense aging) of circulation under.Dilute/dense aging the case where
Under, ageing cycle includes 5 minutes air, 5 minutes N2, 5 minutes 4%H2(surplus N2) and 5 minutes N2；It is straight to repeat the circulation
Reach the required aging duration.
Fig. 4 is provided in air aging at 850 DEG C and the BET after dilute/dense aging 5 hours between comparative example 1 and embodiment 3
The comparison of surface area.Comparative example 1 includes 3.2%CuO, this is the typical load of diesel fuel applications.Embodiment 3 includes 1.7%
CuO is significantly lower than comparative example 1.Under the conditions of air aging, two embodiments all keep BET surface area > 550m2/g.So
And under dilute/dense aging condition, observe the obvious deterioration of the BET surface area of comparative example 1.On the contrary, embodiment 3 is dilute/dense old
It is remained under the conditions of change and the comparable surface area of air aging sample.Table 2 summarizes difference CuO load capacity after dilute/dense aging
The BET surface area of Cu-SSZ-13 and CuSAPO-34.Clearly illustrate lower CuO load capacity in dilute/dense aging condition
Under high thermal stability be it is crucial, this is more relevant with petrol engine (such as poor GDI) application.It can be seen by the data in table 2
Out, the copper load capacity less than about 2.0 weight % or less than about 1.8 weight % is particularly advantageous, because when using such copper negative
When carrying capacity, BET surface area is held essentially constant after weathering.
Table 2
| Zeolite | CuO load capacity (weight %)a | BET surface area (m after aging2/g)b | |
| Comparative example 1 | SSZ-13 | 3.2 | 65 |
| Embodiment 2 | SSZ-13 | 2.4 | 278 |
| Embodiment 3 | SSZ-13 | 1.7 | 578 |
| Embodiment 4 | SSZ-13 | 1.1 | 583 |
| Embodiment 5 | SSZ-13 | 0.6 | 586 |
| Embodiment 6 | SAPO-34 | 1.7 | 569 |
aCu content based on the CuO measured by ICP.
bAs described above, dilute at 850 DEG C/dense aging 5 hours.
Embodiment 8
3 kinds of Cu-CHA catalyst pulps are coated on 1.0 " (diameter) × 3.0 " (length) cylindrical monoliths substrates,
Hole density is 400cpsi (hole count per square inch), and wall thickness is 4 mils.3 kinds of catalyst have different CuO load capacity, such as
Shown in the following table 3.The substrate of coating expansion drying and is calcined 2 hours on circulation drier at 200 DEG C at 450 DEG C.
Table 3
| Catalyst | Cu-CHA CuO load capacity | Carrier coating load capacity, g/in3 |
| A | 3.2 weight % | 3.0g/in3 |
| B | 2.4 weight % | 3.5g/in3 |
| C | 1.7 weight % | 3.5g/in3 |
By 3 kinds of SCR catalysts on horizontal laboratory reactor as described in Example 7 under the conditions of dilute/dense at 850 DEG C
Lower aging 5 hours.Equipped with gas manifold, gas collecting jar with ground-on cover plate and mass flow controller, water pump and evaporator, vertical tubular furnace,
Specimen holder, exhaust gas oxygensensor, thermocouple and MKS MultiGas FT-IR analyzer laboratory reactor on assess SCR performance and
NH3Storage volume.
Two testing schemes are as follows:
I) SCR igniting test: 500ppm NO, 550ppm NH3, 5%H2O, 5%CO2, 10%O2, surplus N2, air speed
(SV)=60K hr-1, T=150-490 DEG C
ii)NH3Storage test: absorption: 500ppm NH3, 5%H2O, 5%CO2, 10%O2, SV=60K hr-1, T=200
℃；Desorption: T=200-490 DEG C
SCR igniting test result is plotted in Fig. 5.Conventional 3.2%Cu-CHA catalyst A is in 300 DEG C or higher temperature
The low NO of the lower generation about 40% of degreexConversion ratio, this shows that SCR component is significantly degraded under given aging condition.On the contrary, identical
After aging process, catalyst B and C with reduced copper content are substantially better than catalyst A.Catalysis with minimum copper load capacity
The SCR activity of agent provides optimal SCR activity.Statistics indicate that this is for gasoline SCR application, especially lean-burn gasoline engines
Using needing lower CuO load capacity.
NH3It is shown in Figure 6 to store test result.Two kinds of catalyst with lower CuO load capacity are desorbed in temperature program(me)
Comparable NH is shown in the process3Storage volume.Catalyst A although CuO load capacity with higher, but shown due to degradation low
Storage volume much.
" embodiment ", " certain embodiments ", " one or more embodiments " are referred to throughout the specification
Or " embodiment " means that specific features, structure, material or characteristic with regard to describing for the embodiment are included at least one
In embodiment of the present invention.The phrase therefore, occurred everywhere throughout the specification such as " in one or more embodiments ",
" in certain embodiments ", it is not necessarily meant to refer to the identical reality of the present invention " in one embodiment " or " in embodiments "
Apply scheme.In addition, specific feature, structure, material or characteristic can be in one or more embodiments with any suitable
Mode combines.
Although describing the present invention by reference to specific embodiment herein, it should be understood that these embodiments are only
To the explanation of principles and applications.It will be apparent to one skilled in the art that not departing from essence of the invention
In the case where mind and range, the method for the present invention and device can be carry out various modifications and changed.Therefore, the present invention is intended to include
Modifications and variations within the scope of the appended claims and their equivalents.
Claims (24)
1. one kind effectively reduces nitrogen oxides (NOx) selective catalytic reduction (SCR) catalyst, the SCR catalyst include with choosing
From the metal promoted molecular sieve of the metal promoted of iron, copper and combinations thereof, wherein metal is with the gross weight based on metal promoted molecular sieve
Amount is calculated as 2.6 weight % with oxide or less amount exists.
2. the SCR catalyst of claim 1, wherein metal exists with about 2.0 weight % or less amount.
3. the SCR catalyst of claim 2, wherein metal exists with about 1.8 weight % or less amount.
4. the SCR catalyst of claim 3, wherein metal exists with about 1.5 weight % or less amount.
5. the SCR catalyst of claim 1, wherein metal exists with the amount of about 0.5 weight % to about 2.5 weight %.
6. the SCR catalyst of claim 1, wherein metal exists with the amount of about 0.5 weight % to about 1.8 weight %.
7. the SCR catalyst of claim 1, wherein metal is copper.
8. the SCR catalyst of claim 1, wherein molecular sieve is maximum ring size and double six rings with eight Tetrahedral atoms
(d6r) small pore molecular sieve of unit.
9. the SCR catalyst of claim 1, wherein molecular sieve is zeolite.
10. the SCR catalyst of claim 9, wherein the structure type of zeolite be selected from AEI, AFT, AFV, AFX, AVL, CHA,
DDR、EAB、EEI、ERI、IFY、IRN、KFI、LEV、LTA、LTN、MER、MWF、NPT、PAU、RHO、RTE、RTH、SAS、SAT、
SAV, SFW, TSC, UFI and combinations thereof.
11. the SCR catalyst of claim 10, wherein structure type is CHA.
12. the SCR catalyst of claim 1, wherein the molar ratio (SAR) of the silica of molecular sieve and aluminium oxide be about 5 to
About 100.
13. the SCR catalyst of claim 1, wherein SCR catalyst shows about 60% after heat ageing processing at 300 DEG C
Or higher NOxConversion ratio, wherein heat ageing processing exists under the conditions of recycling dilute/dense in 10% steam at 850 DEG C
Lower to carry out 5 hours, dilute/dense ageing cycle is by 5 minutes air, 5 minutes N2, 5 minutes 4%H2And surplus is N2With 5 minutes N2Group
At this four steps of repetition are until reaching the aging duration.
14. the SCR catalyst of claim 1, wherein SCR catalyst is shown at least about at 200 DEG C after heat ageing processing
0.60g/L or higher NH3Storage capacity, wherein heat ageing processing is steamed under the conditions of recycling dilute/dense 10% at 850 DEG C
It is carried out 5 hours in the presence of vapour, dilute/dense ageing cycle is by 5 minutes air, 5 minutes N2, 5 minutes 4%H2And surplus is N2With 5 minutes
N2Composition repeats this four steps until reaching the aging duration.
15. a kind of nitrogen oxides (NO effectively reduced in lean-burn gasoline engines exhaust gasx) catalyst article, the catalyst system
Product include the substrate carrier for being provided with carbon monoxide-olefin polymeric, and wherein the carbon monoxide-olefin polymeric includes and appoints in claim 1-14
One SCR catalyst.
16. the catalyst article of claim 15, wherein substrate carrier is honeycomb substrates.
17. the catalyst article of claim 15, wherein honeycomb substrates are metal or ceramics.
18. the catalyst article of claim 15, wherein monolith substrate carrier is flow through substrate or wall-flow filter.
19. the catalyst article of claim 15, wherein the carbon monoxide-olefin polymeric is applied to substrate in the form of carrier coating
On carrier, the carrier coating also includes selected from silica, aluminium oxide, titanium dioxide, zirconium oxide, ceria or combinations thereof
Adhesive.
20. a kind of exhaust treatment system, includes:
Lean-burn gasoline engines generate exhaust gas stream；
Catalyst article, positioned at lean-burn gasoline engines downstream and be in fluid communication with exhaust gas stream, the catalyst article is effective
Nitrogen oxides (NO is reduced from exhaust gas stream in groundx), which includes the substrate for being provided with carbon monoxide-olefin polymeric
Carrier, wherein the carbon monoxide-olefin polymeric includes the SCR catalyst of any one of claim 1-14.
21. the exhaust treatment system of claim 20, also comprising being catalyzed positioned at the lean-burn gasoline engines downstream and the SCR
The three-way conversion catalyst (TWC) of agent upstream and poor NOxAt least one of trap (LNT).
22. the exhaust treatment system of claim 21, wherein one or two of TWC and LNT are in close link position.
23. a kind of method for the exhaust gas stream for handling lean-burn gasoline engines, comprising:
Contact exhaust gas stream and the catalyst article of the substrate carrier comprising being provided with carbon monoxide-olefin polymeric, so that reducing
Nitrogen oxides (NO in exhaust gas streamx), wherein the SCR that the carbon monoxide-olefin polymeric includes any one of claim 1-14 is urged
Agent.
24. the method for claim 23 further includes contacting the exhaust gas stream with one or more catalyst articles, described to urge
Agent product includes the three-way conversion catalyst (TWC) of the upstream positioned at the lean-burn gasoline engines downstream and SCR catalyst
With poor NOxAt least one of trap (LNT).
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| US201762462151P | 2017-02-22 | 2017-02-22 | |
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| PCT/IB2018/051076 WO2018154463A1 (en) | 2017-02-22 | 2018-02-21 | Exhaust gas treatment catalyst for abatement of nitrogen oxides |
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| JP6693406B2 (en) * | 2016-12-20 | 2020-05-13 | 三菱自動車工業株式会社 | Exhaust gas purification device |
| PL3687667T3 (en) | 2018-01-08 | 2023-06-26 | Pacific Industrial Development Corporation | Catalyst comprising ceria-zirconia-oxygen storage material and process for its production |
| CN112166213A (en) | 2018-04-04 | 2021-01-01 | 尤尼弗瑞克斯 I 有限责任公司 | Activated porous fibers and products including the same |
| WO2020055133A1 (en) | 2018-09-11 | 2020-03-19 | 주식회사 엘지화학 | Interface unit |
| JP7294620B2 (en) | 2018-09-11 | 2023-06-20 | エルジー エナジー ソリューション リミテッド | interface unit |
| US11187127B2 (en) | 2019-06-28 | 2021-11-30 | Deere & Company | Exhaust gas treatment system and method with four-way catalyzed filter element |
| EP3885029A1 (en) * | 2020-03-24 | 2021-09-29 | UMICORE AG & Co. KG | Platinum and zinc-containing zeolite |
| KR102204973B1 (en) | 2020-08-25 | 2021-01-19 | 최우석 | Ceramic honeycomb honeycom filter modul and ventilation system |
| JP2024505922A (en) * | 2021-02-02 | 2024-02-08 | ビーエーエスエフ コーポレーション | NH3 reduction catalyst for mobile gasoline applications |
| CN113842943B (en) * | 2021-09-26 | 2023-03-14 | 中国科学院山西煤炭化学研究所 | B-doped Cu-SSZ-13 molecular sieve and preparation method and application thereof |
| WO2024008628A1 (en) * | 2022-07-04 | 2024-01-11 | Basf Corporation | An exhaust gas treatment system for treating an exhaust gas stream exiting a gasoline engine |
| GB2622259A (en) * | 2022-09-09 | 2024-03-13 | Edwards Ltd | NOx reduction |
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